US9475780B2 - Process for the synthesis of cyclic alkylene ureas - Google Patents

Process for the synthesis of cyclic alkylene ureas Download PDF

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US9475780B2
US9475780B2 US14/233,302 US201214233302A US9475780B2 US 9475780 B2 US9475780 B2 US 9475780B2 US 201214233302 A US201214233302 A US 201214233302A US 9475780 B2 US9475780 B2 US 9475780B2
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carbonate
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carbon atoms
cyclic
alkylene
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US20140163221A1 (en
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Ram Gupta
Irina Kobylanska
Urvee Treasurer
Lawrence Flood
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Allnex Netherlands BV
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D243/00—Heterocyclic compounds containing seven-membered rings having two nitrogen atoms as the only ring hetero atoms
    • C07D243/04—Heterocyclic compounds containing seven-membered rings having two nitrogen atoms as the only ring hetero atoms having the nitrogen atoms in positions 1 and 3
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D233/00—Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings
    • C07D233/04—Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
    • C07D233/28—Heterocyclic compounds containing 1,3-diazole or hydrogenated 1,3-diazole rings, not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D233/30—Oxygen or sulfur atoms
    • C07D233/32—One oxygen atom
    • C07D233/34—Ethylene-urea
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D239/00—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings
    • C07D239/02—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings
    • C07D239/06—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member
    • C07D239/08—Heterocyclic compounds containing 1,3-diazine or hydrogenated 1,3-diazine rings not condensed with other rings having one double bond between ring members or between a ring member and a non-ring member with hetero atoms directly attached in position 2
    • C07D239/10—Oxygen or sulfur atoms

Definitions

  • the invention relates to a process for the synthesis of cyclic alkylene ureas, and to the products obtained from this process.
  • the reaction can be carried out under anhydrous conditions or in presence of water and/or a high boiling solvent such as ethylene glycol and diethylene glycol, however, the beneficial use of water in markedly increasing the yield versus reactions conducted under anhydrous conditions is noted and exemplified.
  • Water is believed to be responsible for the more complete conversion of the intermediate condensation product to ethylene urea.
  • the crude ethylene urea thus formed does not form a clear solution in water but results in turbid solutions which are distinctly alkaline, while pure ethylene urea is fully soluble in water.
  • the desired product ethylene urea is generally isolated from the aqueous solution by crystallisation as hemihydrate, and comprises a mass fraction from about 5% to 15% of water.
  • Some of the disadvantages of this process route using urea as a reactant are the formation of water-insoluble by-products, the need to react at higher temperature and higher pressure conditions, and formation of hydrated ethylene urea which is not a free-flowing powder, but has a propensity to cake and form lumps.
  • the object of the invention is therefore a process for the synthesis of cyclic alkylene ureas by reacting a difunctional aliphatic amine A having two primary amino groups, and an aliphatic organic carbonate component C selected from the group consisting of dialkyl carbonates CD and of alkylene carbonates CA, wherein the ratio of the amount of substance n(—NH 2 ) of primary amino groups —NH 2 in the difunctional amine A to the sum n(C) of the amount of substance n(CD) of carbonate groups of the dialkyl carbonate CD and the amount of substance n(CA) of carbonate groups of the alkylene carbonate CA, is at least more than 2.
  • This reaction is conducted in the presence of a basic catalyst which is preferably selected from the group consisting of alkoxides of alkali metals of group 1 of the Periodical System of Elements, and of alkoxides of earth alkali metals, of group 2 of the Periodical System of Elements, according to recent IUPAC nomenclature, and of mixtures thereof.
  • a basic catalyst which is preferably selected from the group consisting of alkoxides of alkali metals of group 1 of the Periodical System of Elements, and of alkoxides of earth alkali metals, of group 2 of the Periodical System of Elements, according to recent IUPAC nomenclature, and of mixtures thereof.
  • a primary difunctional amine in the context of this invention, has exactly two primary amino groups.
  • the preferred difunctional amines A have two primary amino groups attached to a linear or branched or cyclic aliphatic structure which preferably has from two to twenty carbon atoms.
  • the two amino groups in the same molecule of a difunctional amine A are separated from each other by at least two successive carbon atoms.
  • One or more of the carbon atoms may be separated by an oxygen atom in an ether bond, —C—O—C—, where any two oxygen atoms are preferably separated by two carbon atoms, forming a structure —C—O—C—C—O—C—.
  • One or more of such oxygen atoms may be replaced by a sulphur atom.
  • Preferred diprimary diamines A are ethylenediamine, 1,2-diaminopropane, 1,3-diaminopropane, 1,4-diaminobutane, 2,3-diaminobutane, 1,5-diaminopentane, 1,2-diaminocyclohexane, 1,6-diaminohexane, bis-(2-aminoethyl) ether, 1,12-diamino-4,9-dioxadodecane, and a mixture of 2,2,4- and 2,4,4-trimethyl-1,6-diaminohexane.
  • Particularly preferred difunctional amines are 1,2-diaminoethane, 1,2- and 1,3-diaminopropane, 1,4- and 2,3-diaminobutane, as well as mixtures of these.
  • the amine A is has the structure H 2 N—CR 1 R 2 —(CR 3 R 4 ) n —(CR 5 R 6 ) m —CR 7 R 8 —NH 2 , where any of the radicals R i with i ranging from 1 to 8 may independently from any other of the said radicals be H, an alkyl group having from one to eight carbon atoms and being linear branched or cyclic, an alkenyl group having at least one olefinic unsaturation and from one to eight carbon atoms and being linear branched or cyclic, an alkoxy group having from one to eight carbon atoms and being linear branched or cyclic, or a carboxyl or carboxyl ester group, and n and m may independently be 0 or 1.
  • R 3 , R 4 , R 5 , and R 6 may also be a halogen atom, or a hydroxyl group.
  • a C-substituted ethylene urea is the reaction product, e.g., a 4,4-dialkyl ethylene urea or a 4,5-dialkyl ethylene urea, a 4-vinyl ethylene urea or a 4-methoxy ethylene urea.
  • a C-substituted propylene urea is obtained such as, e.g., 4-methyl propylene urea, 5-halogen propylene urea, 5-hydroxy propylene urea, 5,5-dimethylpropylene urea, 5-carboxypropylene urea, the ethyl ester of propylene urea-5-carboxylic acid, and 5-methoxy propylene urea.
  • a C-substituted butylene urea is obtained such as 5-hydroxybutylene urea, 5,6-dihydroxybutylene urea, 4-alkyl butylene urea, 4,5,6,7-tetraalkyl butylene urea, and 4,7-dimethylbutylene urea.
  • the aliphatic organic carbonate component, C can be an alkylene carbonate CA, or a dialkyl carbonate, CD, or a mixture of these.
  • Alkylene carbonates CA are cyclic esters of dihydroxyalkanes preferably having from two to six carbon atoms, such as ethylenecarbonate, 1,2- and 1,3-propylenecarbonate.
  • Useful alkylene carbonates are ethylenecarbonate and 1,2-propylenecarbonate, which are both commercially available.
  • Dialkyl carbonates CD have the structure R a —O—CO—O—R b , where R a and R b may be the same, or may be different, and may independently be selected from the group consisting of linear and branched alkyl radicals having from one to twelve carbon atoms. Especially preferred are dimethyl carbonate, and diethyl carbonate, and mixtures of these.
  • Basic catalysts which have proved to be useful for the invention are preferably alkali metal or earth alkali metal alkoxides, particularly preferred, lithium methoxide, sodium methoxide and potassium methoxide, or the ethoxides of lithium, sodium, and potassium, and mixtures of these.
  • alkali alkoxides or earth alkali alkoxides may be generated in situ, such as from an alkanol and an alkali or earth alkali hydroxide, preferably under removal of water, or by reaction of an alkali or earth alkali metal, their amides, or their hydrides, with an alkanol.
  • n(—NH 2 )/n(C) of the amount of substance n(—NH 2 ) of primary amino groups —NH 2 in the aliphatic amine A to the sum n(C) of the amount of substance n(CD) of carbonate groups of dialkyl carbonate CD and the amount of substance n(CA) of carbonate groups in alkylene carbonate CA present in the carbonate component, C, is at least more than 2, in accordance with the invention: n (—NH 2 )/ n (C) ⁇ n (—NH 2 )/[ n (CD)+ n (CA)]>2.
  • this ratio n(—NH 2 )/n(C) is at least 2.2, particularly preferably, at least 2.4, and with special preference, at least 2.5. Good results have also been obtained when the ratio is at least three, or with more preference, at least four.
  • a diprimary diamine such as ethylenediamine or 1,3-diaminopropane
  • a carbonate compound a cyclic urea having two amidic N—H groups is formed, in this case, ethyleneurea or propyleneurea.
  • the process according to the invention preferably comprises the following steps:
  • a mixture of solvent, difunctional amine A, and preferably, also catalyst is charged into a reactor, and the carbonate component C is added preferably over a time span of between fifteen minutes and six hours, under mixing conditions such as stirring, or circulating the reaction mixture in a tubular loop which includes at least one mixing section which may be a nozzle set into a tube, or a static mixer.
  • Another process that can be used comprises therefore the following steps:
  • the difunctional amine A, the carbonate C, and the catalyst may be charged in any order to a reaction vessel. If a solvent is used, it may be charged before addition of the reactants and catalyst, or may be added together with any of these, or may be added last. It is preferred to at least partially replace the air by nitrogen or an other inert gas.
  • the reaction mixture is preferably heated, and continued until the reaction is essentially complete, as evidenced by samples drawn from the reaction mixture.
  • the alcohol released from the carbonate component C, and excess amine A may then be removed, preferably by distillation under reduced pressure.
  • the cyclic alkylene urea formed is then isolated.
  • the reaction product is preferably isolated as a precipitate by filtration, before or after removal of the excess amine, and the alcohol is preferably removed by distillation under reduced pressure. The precipitate may then be washed with further solvent. If a solvent is used, and the cyclic alkylene urea is significantly soluble in the solvent, the cyclic alkylene urea may be recovered by partially or completely removing the solvent, or it may be precipitated from the solution by adding a non-solvent, or a combination of both processes.
  • a substance is called “not soluble” in a specified solvent if it is not significantly soluble in this solvent, at ambient temperature (20° C.).
  • not significantly soluble it is meant that the mass fraction of the substance in question dissolved in a solvent which is in equilibrium with the substance in question is preferably not more than 10%.
  • the washed precipitate usually has a purity of more than 90%.
  • further washing steps, recrystallisation, melt crystallisation, or dissolution of the cyclic alkylene urea in water to form a solution which may be purified by ion exchange or adsorption methods can be preferably used. Residual unreacted difunctional amine can be removed by treatment with ion exchange resins.
  • the most preferred process is conducted by charging the amine A, the carbonate component C, and the catalyst to a reaction vessel, optionally adding a solvent as detailed infra, optionally, at least partially replacing the air by nitrogen or an other inert gas, and holding the mixture at a reaction temperature of between 0° C. to 250° C.
  • the upper temperature limit is preferably chosen to allow reflux, or support fractional distillation to separate the cyclic urea from reaction byproducts.
  • the basic catalyst can be added together with the reactants, or preferably, is slowly added to the mixture of reactants as charged, or to the pre-heated reactants, preferably during a period of between ten minutes and sixty minutes, under stirring. Heating and stirring the reaction mixture is then continued until the reaction has proceeded to essential completion, as shown by the amount of alcohol or diol formed from the carbonate component, C, then separating the excess amine A and alcohol or diol released from the carbonate component C by distillation under reduced pressure, filtering of the residue, and isolating of the cyclic alkylene urea formed.
  • a solvent can be added to the reactants, which solvent is selected from the group consisting of aliphatic linear, branched or cyclic alcohols having from one to eighteen carbon atoms, such as n-butanol or isopropanol, aliphatic glycols having a linear or branched alkylene chain of from two to six carbon atoms, such as ethylene glycol or 1,2-propylene glycol, monoalkyl ethers of any of the alcohols, where the alkyl groups have from one to four carbon atoms, monoalkyl ethers or dialkyl ethers of any of the preceding where the alkyl groups independently have from one to four carbon atoms, such as methoxypropanol, ethoxybutanol, or 1,4-dimethoxybutane, and of alkyl aromatic compounds or mixtures thereof, such as toluene, xylene, ethyl benzene, and methyl naphthalen
  • the excess difunctional amine A and the alcohol formed in the reaction is removed by, e.g., distillation under reduced pressure.
  • the alkylene urea usually solidifies, or separates from the solvent if a solvent is present.
  • solvent is chosen to dissolve the alkylene urea only slightly or not at all.
  • Aliphatic ethers like dimethoxyethane or alkyl aromatic compounds such as toluene or xylene or mixtures of these optionally with mesitylene and cumene which are sold as “solvent naphtha” are particularly suitable.
  • An important advantage of the process claimed is the essential absence of water in the reaction which leads to the low level of water in the final product.
  • the cyclic urea is solid at ambient temperature (20° C.), such as ethylene urea and propylene urea
  • this process allows to obtain the cyclic urea as a free-flowing solid, and also, in the form of free-flowing prills, with little or no propensity to form aggregates.
  • the mass fraction of water in the final product is not more than 5%, and is preferably found to be not more than 1%.
  • FTIR Infrared spectra were acquired using a DuraScope single reflection diamond ATR accessory mounted in the sample chamber of a Digilab 7000e FTIR spectrometer.
  • “Purity” is the ratio of the mass of the desired product to the mass of the material used (when used as starting material) or obtained (when present in the reaction product), usually measured in “%”, or cg/g.
  • “Strength” is the mass fraction w B of solute B in a solution S, calculated as the ratio of the mass m B of solute B and the mass m S of the solution, usually measured in “%”, or cg/g.
  • Yield is the ratio of the mass of the desired reaction product obtained in a chemical reaction or a physicochemical process, and the expected mass of the reaction product without any loss due to side reactions or lost product during isolation thereof.
  • a product was prepared by the following procedure according to the invention:
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C. to remove methanol and other volatile materials, and the precipitate was washed with acetone.
  • the resulting product was analysed by 13 C-NMR and found to be ethylene urea with a purity of 94% and a yield of 80%.
  • the isolated product had a mass fraction of water of less than 1% as determined by Karl Fischer-titration, and a mass fraction of residual ethylenediamine of 250 mg/kg, as determined by GC-MS.
  • a product was prepared by the following procedure according to the invention:
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C. to remove methanol and other volatile materials, and the precipitate was washed with acetone.
  • the isolated product was analysed by 13 C-NMR and found to be ethylene urea, with a purity of 89%, in a yield of 81%.
  • a product was prepared by the following procedure according to the invention:
  • a white precipitate was formed upon cooling the reaction mixture.
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C. to remove methanol and other volatile materials, and the precipitate was washed with acetone.
  • the isolated product was analysed by infrared spectroscopy and found to be ethylene urea in a yield of 80%, having a mass fraction of water of less than 1%.
  • a product was prepared by the following procedure according to the invention:
  • the isolated product was analysed by 13 C-NMR spectroscopy, and found to be ethylene urea. Its melting temperature was 135° C., and the mass fraction of water was found to be 0.4% by Karl Fischer-titration. The yield was 90%.
  • a product according to the invention was prepared by the following procedure:
  • a product according to the invention was prepared by the following procedure:
  • the isolated product was analysed by 13 C-NMR and found to be ethylene urea with purity of 97%, with a mass fraction of water of 0.4% as measured by Karl Fischer-titration.
  • the mass fraction of residual ethylenediamine was found to be 150 mg/kg.
  • the melting temperature of the ethylene urea formed was 135° C.
  • the yield was 90%.
  • a product having a purity of 99.9% and a mass fraction of residual ethylenediamine of 100 mg/kg was obtained.
  • the product was a free-flowing solid.
  • a product according to the invention was prepared by the following procedure:
  • the isolated product was analysed by 13 C-NMR and found to be ethylene urea with purity in excess of 97%.
  • a product was prepared by the following procedure according to the invention:
  • reaction mixture started to reflux, the mixture was then held for two hours under reflux and then, a white precipitate was formed upon cooling of the reaction mixture.
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C. to remove methanol and other volatile materials, and the precipitate was washed with methyl isobutyl ketone.
  • the isolated product was analysed by GC/MS and found to be ethylene urea.
  • a product was prepared by the following procedure according to the invention:
  • the isolated product was analysed by 13 C-NMR, and found to be ethylene urea with presence of residual ethylene glycol.
  • a product was prepared by the following procedure:
  • This material was diluted with acetone and filtered. The remaining solid compound was analysed by infrared spectroscopy, and no significant amount of ethylene urea was found. Unlike the product of Example 1, this product was only partially soluble in water, and had melting temperature above 150° C.
  • a product was prepared by the following procedure:
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C., and the remaining solids were washed with acetone.
  • the product was analysed by infrared spectroscopy and no ethylene urea was found.
  • the product was only partially water soluble, having a melting temperature of 250° C.
  • a product was prepared by the following procedure:
  • the reaction mixture was concentrated by distillation under reduced pressure (25 kPa) at 95° C. The remaining product was analysed by infrared spectroscopy, and no ethylene urea was found. The product of this reaction is not water soluble, but acetone soluble.
  • a compound was prepared by the following procedure:
  • the temperature was then increased to 120° C., and held for two hours. A white precipitate containing almost no solvent was formed. The remaining product was not water-soluble and not acetone soluble, with a melting temperature in excess of 200° C. No significant amount of ethylene urea was found.
  • a product according to the invention was prepared by the following procedure:

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  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
US14/233,302 2011-07-20 2012-07-19 Process for the synthesis of cyclic alkylene ureas Active 2032-10-01 US9475780B2 (en)

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EP11174656 2011-07-20
EP11174656.6 2011-07-20
EP11174656A EP2548870A1 (en) 2011-07-20 2011-07-20 Process for the Synthesis of Cyclic Alkylene Ureas
PCT/US2012/047305 WO2013012991A1 (en) 2011-07-20 2012-07-19 Process for the synthesis of cyclic alkylene ureas

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US10336681B2 (en) * 2015-03-23 2019-07-02 Council Of Scientific & Industrial Research Process for the synthesis of dialkyl carbonates
US11919866B2 (en) 2017-08-11 2024-03-05 Nouryon Chemicals International B.V. Process for preparing cyclic alkylene ureas

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EP2548869A1 (en) * 2011-07-20 2013-01-23 Cytec Technology Corp. Process for the Synthesis of N-substituted Cyclic Alkylene Ureas
CN103497157B (zh) * 2013-10-16 2015-01-21 厦门大学 一种2-咪唑烷酮的合成方法
WO2017005924A1 (de) * 2015-07-08 2017-01-12 Byk-Chemie Gmbh Urethan- und harnstoffgruppenhaltige reaktionsprodukte
CN114890950B (zh) * 2022-05-16 2023-08-11 中国科学院过程工程研究所 一种2-咪唑烷酮的制备方法
CN117126109B (zh) * 2023-10-26 2024-03-15 中南大学 一种甲醛去除剂、及其制备方法和应用

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US11919866B2 (en) 2017-08-11 2024-03-05 Nouryon Chemicals International B.V. Process for preparing cyclic alkylene ureas

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